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A method for continuously producing high-quality needle coke

A technology of needle coke and raw coke, applied in coking ovens, coking carbonaceous materials, petroleum industry, etc., can solve the problem that the coke pulling effect of the bulk mesophase cannot be achieved, the shear force is small, and the microstructure of needle coke cannot be realized uniaxial orientation, etc.

Active Publication Date: 2021-03-30
CHINA UNIV OF PETROLEUM (EAST CHINA)
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  • Abstract
  • Description
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AI Technical Summary

Problems solved by technology

The above-mentioned technology adopts the degassing coke-pulling process to prepare needle coke, and the released gas is defined by the pressure generated by the self-produced gas of the raw material oil. The amount of gas produced is different. For example, the gas amount in the later stage of mesophase development is much smaller than that produced by the violent cracking of raw oil in the early stage of the reaction. In most cases, the shear force generated by the escape of light components in the late stage of development Small, the ideal coke effect cannot be achieved for the bulk mesophase in the system, resulting in the needle coke microstructure unable to achieve uniaxial orientation
In addition, the above two similar patents are both batch processes, and there is currently a lack of a continuous process for producing high-quality needle coke (ie, high mesophase content and highly uniaxially oriented mesophase structure)

Method used

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  • A method for continuously producing high-quality needle coke

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Effect test

Embodiment 1

[0024] The high-temperature coal tar is used as the feed material of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 18 hours, and the reaction temperature is 420°C. The pulse reaction process is regulated during the reaction residence time. That is, the reaction starts to control the high pressure of 1MPa for 3 hours, the pressure drops to 0.1MPa for 3 hours, then the pressure rises to 1MPa for 3 hours, then the pressure drops to 0.1MPa for 3 hours, and then the pulse reaction process is continuously carried out as a cycle. Continuous feed during the process until the end of the reaction cycle; after the reaction, the green coke is quickly transferred out of the carbonization reactor, the yield of green coke is 55.9%, the yield of liquid by-products is 35.3%, and the yield of gas by-products is 8.8% . The mesophase content of the obtained green coke is 1...

Embodiment 2

[0026] The low-temperature coal tar is used as the feed material of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 20 h, and the reaction temperature is 430 ° C. During the reaction residence time, the pulse reaction process is regulated. That is, the reaction starts to control high pressure 2MPa for 3 hours, the pressure drops to 1MPa for 3 hours, then the pressure rises to 2MPa for 3 hours, then the pressure drops to 1MPa for 3 hours, and then the pulse reaction process is continuously carried out as a cycle. Continuous feeding until the end of the reaction cycle; after the reaction, the green coke was quickly transferred out of the carbonization reactor, the yield of green coke was 58.7%, the yield of liquid by-products was 33.0%, and the yield of gas by-products was 8.3%. The mesophase content of the obtained green coke is 95%, and it is in the form o...

Embodiment 3

[0028]The vacuum residue is used as the feed of the continuous process, and the raw material enters the carbonization reactor 2. Under the protection of nitrogen, the total residence time of the reaction raw material is 19h, and the reaction temperature is 435°C. The pulse reaction process is regulated during the reaction residence time , that is, the reaction starts to control the high pressure 2MPa for 2.5h, the pressure drops to 1.5MPa for 2.5h, then the pressure rises to 2MPa for 2.5h, then the pressure drops to 1.5MPa for 2.5h, and then continues to use this as a cycle Pulse reaction process, continuous feed during the reaction until the end of the reaction cycle; after the reaction, the green coke is quickly transferred out of the carbonization reactor, the yield of green coke is 60.5%, the yield of liquid by-products is 33.2%, and the yield of gas by-products The yield was 6.3%. The mesophase content of the obtained green coke is 100%, and it is in the shape of oriented...

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Abstract

The invention discloses a method for continuously producing high-quality needle coke. The method mainly comprises the following steps that 1, raw materials are pressurized by a metering pump through aheating furnace tube and then continuously enter a carbonization reactor (high-pressure coke tower), the temperature in the carbonization reactor is maintained to be 400-500 DEG C, feeding continuesfor 10-24 hours, then feeding is stopped, and the reaction continues for 0-18 hours; in the whole carbonization reaction process, high pressure-low pressure alternate pulse operation is used in the carbonization reactor, the reaction pressure changes in the range of 1.0-6.0 MPa; 2, green coke generated at the bottom of the carbonization reactor is removed through hydraulic decoking and dischargedfrom the bottom of the carbonization reactor; 3, the green coke product is calcined at 1450 DEG C for 2-4 hours to obtain the coke. The method is beneficial to formation of needle coke products of theoptical structure in a highly uniaxial orientation fine fiber shape, the interphase content is up to 95% or above, and the CTE, measured at 25-600 DEG C, of a graphite electrode prepared from the needle coke is smaller than or equal to 1.3*10<-6> / DEG C. Meanwhile, the process has the advantages of being simple in process flow, high in operability and capable of achieving continuous production.

Description

technical field [0001] The invention designs the field of high-grade carbon material production technology, especially a continuous process for producing high-quality needle coke. Background technique [0002] Needle coke is a kind of carbon material with many uses. It has a silver-gray metallic luster on the outside. The section of raw coke has a fine fiber-like uniaxial distribution optical texture. Features, high-power electrodes and ultra-high-power electrodes made of it have small resistivity, strong thermal shock resistance, and high mechanical strength. As a high-quality carbon material, it is widely used in electric arc furnace steelmaking. In the smelting industry, the smelting efficiency can be increased by more than 3 times. With the vigorous development of my country's iron and steel industry, the demand for needle coke is also increasing day by day. According to incomplete statistics, my country needs about 200,000 tons of needle coke products every year. However,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10B55/00
CPCC10B55/00
Inventor 刘东龚鑫娄斌于冉
Owner CHINA UNIV OF PETROLEUM (EAST CHINA)